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Mass Transfer

Mass Transfer
The film penetration model of mass transfer was enunciated by

Gilliland
Toor and Marchello
Stefan
Fick

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Mass Transfer
In case of absorption & stripping, the interface of the liquid & gas phases are present in equilibrium, when the diffusional resistance of __________ is zero.

Gas phase
Interface
Liquid phase
All of these

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Mass Transfer
Absorption (liquid-gas system) with evolution of heat as compared to isothermal absorption results in

All of these
Decreased solute solubility
Large number of trays
Large minimum liquid to gas (L/G) ratio

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Mass Transfer
Azeotropic distillation is employed to separate

Mixture with very high relative volatility
Heat sensitive materials
Constant boiling mixture
High boiling mixture

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Mass Transfer
Extraction of pencillin employs a __________ extraction coloumn.

Centrifugal
None of these
Packed
Plate

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Mass Transfer
H₂S is being absorbed in a gas absorber unit. The height of the transfer unit based on the overall mass transfer coefficient on the gas side is 0.4 m. The equilibrium data is given by, y = 1.5 x. The bulk concentration of H₂S has to be reduced from 0.05 to 0.001 mole fraction in the gas side. The height of the tower (in metres) corresponding to an operating line given by, y = 5x + 0.001 is

0.56
1
1.56
2

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